Porous membrane and process for preparing the same

ABSTRACT

The present invention relates to a porous membrane including cellulose fibers, wherein the surface area determined by congo red coloring of the re-dispersed cellulose fibers after the cellulose fibers of the porous membrane are re-dispersed in accordance with the re-dispersion method for normal paper specimens according to JIS P 8120 is from 100 to 300 m 2 /g. The porous membrane according to the present invention can provide a separator for electrochemical devices with superior properties, at a reasonable cost.

TECHNICAL FIELD

Priority is claimed on Japanese Patent Application No. 2011-226270, filed on Oct. 13, 2011, the content or which is incorporated herein by reference.

The present invention relates to a porous membrane and a process for preparing the same. In particular, the present invention relates to a porous membrane formed from cellulose suitable for a separator for an electrochemical device and a process for preparing the same.

In the specification of the present application, an electrochemical device means an electrochemical device equipped with a positive electrode, a negative electrode, and a separator. As examples thereof, mention may be made of, for example, various types of secondary batteries such as a lithium ion secondary battery and a polymer lithium battery; various types of capacitors such as an aluminum electrolytic capacitor, an electrical double-layered capacitor and a lithium ion capacitor; and the like.

BACKGROUND ART

Recently, use of electricity as a source of energy has increased for addressing environmental problems related to CO₂ reduction, depletion of fossil fuel resources and the like. Therefore, for example, electric vehicles utilizing secondary batteries are being actively developed in the automobile industry. In addition, secondary batteries are featured also in view of efficient use of natural energy such as solar or wind energy.

In general, lithium ion secondary batteries are used as the secondary batteries for driving electric vehicles, at present, in view of the relationship between power and energy density. On the other hand, various companies have focused on the development of next-generation batteries in view of increased energy density, output, safety and the like. The next-generation batteries are in the fields with high future growth in the market.

On the other hand, in secondary batteries other than lithium ion secondary batteries, primary batteries, capacitors (condensers) and the like, separators formed from paper, non-woven fabrics, porous films or the like are used. The performances required for the separators are, in general, short circuit protection between positive and negative electrodes, chemical stability with respect to electrolytic solutions, low inner resistivity and the like. The aforementioned requisite performances are universal ones required in separators regardless of types thereof, although they differ in degree in accordance with devices.

Separators of almost all lithium ion secondary batteries use porous membranes formed from a polymer organic compound such as polypropylene, polyethylene or the like. The aforementioned porous membranes possess some characteristics suitable for lithium ion secondary batteries. For example, the following characteristics can be mentioned.

(1) Chemical stability with respect to electrolytic solutions is exhibited, and no fatal failures occur by separators. (2) Thickness of a separator can be freely designed, and for this reason, separators responding to various demands can be provided. (3) The diameter of pores can be designed to be reduced, and for this reason, superior lithium shielding properties are exhibited, and short circuit caused by lithium dendrite hardly occurs. (4) When thermal runaway of lithium ion secondary batteries occurs, the initial thermal runaway can be controlled by melting polypropylene or polyethylene and thereby narrowing pores.

However, conventional research for lithium ion secondary batteries cannot identify an underlying cause of an occurrence of thermal runaway. Various companies have studied and proposed a means for avoiding risks of thermal runaway of various materials used in secondary batteries by empirical tools, under present circumstances. Developments of materials suitable for vehicles having increased safety are considered by clarifying the principle of thermal runaway and establishing a common evaluation method thereof hereafter. Problems with respect to safety are expected to be overcome.

On the other hand, the second problem in secondary batteries for use in vehicles is cost. A separator is a material accounting for 20% of the battery cost, and further cost reduction is required under the present circumstances.

For example, in the field of rechargeable transportation units such as electric vehicles, and in the field of portable electronic terminals such as mobile phones, an electrical energy-storage device having an increased amount of storage electrical energy per unit volume is required in order to be operational for a long period of time even with a reduced volume. As an example of the aforementioned electrical energy-storage device, mention may be made of an electrical double-layered capacitor in which an electrolyte dissolved in an electrolytic solution is adsorbed by an electrode, and electrical energy is stored on the interface (electrical doable layer) formed between the electrolyte and the electrode.

Main roles of separators in the electrical double-layered capacitors are short circuit protection of electrodes (separatability), non-blocking movement of ions in the electrolytic solution (low inner resistivity), and the like. However, the aforementioned porous membranes have high density, and for this reason, the inner resistivity tends to increase. On the other hand, it is known that non-woven fabrics are used as a separator of a capacitor, but there are problems in that when a fiber diameter is reduced or a fiber density is increased in order to maintain separatability, an inner resistivity increases. For this reason, development of a separator with a reduced inner resistivity is desirable.

There are two major processes for preparing polymer porous membranes of polypropylene, polyethylene or the like, namely a wet process and a dry process. The aforementioned preparation processes have respective characteristics. In the wet process, a plasticizer is added to a polymer such as polyethylene to form a film, subsequently, the film is biaxially drawn, the plasticizer is removed by cleaning with a solvent, and thereby, pores are provided. In this process, there are advantages in that pore size or film thickness can be superiorly adjusted, and response to various demands for all individual types of batteries can be carried out. On the other hand, there is a problem in that the preparation process is complicated, and for this reason, cost increases. In contrast, in the dry process, a polymer such as polyolefin is dissolved, the polymer is extruded on a film, the film with the polymer is subjected to annealing, the annealed film is drawn at a low temperature to form pores at the initial stage, and subsequently, drawing at a high temperature as carried out to form a porous product. In this process, there are advantages in that polymers having different melting points can be laminated, and the process is easy, and for this reason, the product can be produced at a reasonable cost. On the other hand, there is a problem in that sensitive adjustment of pores or thickness cannot be carried out.

A separator using non-woven fabrics formed from synthetic fibers, inorganic fibers or the like, other than the polymer porous films, has also been proposed. Conventional non-woven fabrics include dry types of non-woven fabrics and wet types of non-woven fabrics, and both of these have also been utilized as separators. It is believed that dry types of non-woven fabrics by which uniformity of fiber distribution cannot be obtained has a low effect of isolating electrodes, and for this reason, they cannot be used for lithium ion secondary batteries. On the other hand, wet types of non-woven fabrics have characteristics in that fiber distribution is uniform, as compared with dry types of non-woven fabrics. In addition, a higher porosity can be adjusted, as compared with porous films due to the characteristics of the preparation process, and for this reason, a sheet with reduced impedance can be produced. However, it is substantially difficult to use the dry types of non-woven fabrics in batteries using graphite negative electrodes which are widely applied to lithium ion secondary batteries at present. This is due to the characteristics of lithium ion secondary batteries which produce lithium dendrite at the negative electrode side. The aforementioned lithium dendrite has a property in which lithium dendrite is easily produced on the surface of a negative electrode which many lithium ions in a separator pass. For this reason, in non-woven fabrics in which roughness in a range with several dozen μm order is formed in the sheet itself, the parts at which lithium dendrite is easily formed are course. Therefore, shielding properties of controlling short circuit at the time of producing lithium dendrite may be reduced, as compared with a film type one.

In order to overcome the aforementioned problems, specifying a pore size to a specified range is carried out, as described in Patent Document 1 (Japanese Unexamined Patent Application, First Publication No. H11-040130). However, the pore size depends on a fiber diameter. For this reason, the fiber diameter needs to be reduced in order to control the pore size to a small size. In the present technology, it is difficult to produce fibers with a nano-order size at a reasonable cost. For this reason, even if synthetic fibers which are referred to as ultrafine fibers are used, it is substantially impossible to control the pore size to a size suitable for a lithium ion secondary battery. Therefore, lithium shielding properties cannot be improved.

In addition, a method for producing a non-woven fabric using an electrostatic spinning method as described in Patent Document 2 (Japanese Patent No. 4425576) is proposed. However, the aforementioned method may not be a realistic method, considering production efficiency and that it is substantially difficult to prepare a sheet having a thickness of several dozen micrometers in present production facilities.

On the other hand, many separators of cellulose type are proposed. For example, Patent Document 3 (Japanese Patent No. 4201308) describes that since the hydroxyl groups of cellulose are not electrochemically stable, an acetylation treatment is carried out, and thereby, the hydroxyl groups are stabilized to nave an aptitude of a lithium ion secondary battery. However, a separator mainly having cellulose has been used in trials of some lithium ion secondary batteries. For this reason, electrochemical stability of cellulose per se in a lithium ion secondary battery may not be a problem.

Patent Document 4 (Japanese Patent No. 4628764) also proposes a separator using cellulose nanofibers. Only cellulose fibers having a thickness of 1,000 nm or less described in Patent Document 3 are reliably obtained in accordance with a method of utilizing bacteria cellulose as described in Patent Document 4 or the like. However, a method of industrially obtaining cellulose fibers by using bacteria cellulose is not established, and a production cost is unclear. Therefore, the aforementioned method may not be an effective means for producing a sheet at a reasonable cost. In addition, Patent Document 4 also describes a means of utilizing natural cellulose. When natural cellulose is treated to uniformly have a thickness of 1,000 nm or less, fibrillation proceeds. Thereby, properties of maintaining water are increased, viscosity is greatly increased as a raw material for papermaking, and poor efficiency of dehydration is exhibited. For this reason, the aforementioned method may not be an effective means. In addition, Patent Document 4 also describes that the production can also be carried out by a casting method, but the process of forming pores is different from that in papermaking. Nevertheless, Patent Document 4 fails to clearly describe a means therefor or provide a sufficient description therefor.

In addition, papermaking is carried out by using a filter fabric or mesh in a step of forming a sheet. In accordance with this method, the filter fabric face is transferred during dehydration, and for this reason, irregularities of several micrometers are formed at the transferred face side. Therefore, when the separator is incorporated in a lithium ion secondary battery, insufficient adhesion between the separator and electrodes is exhibited, and battery performance may be degraded. Therefore, this is not preferable.

Patent Document 5 (Japanese unexamined Patent Application, First Publication No. 2010-090486) proposes a sheet in which an oil-based compound is emulsified using fine cellulose fibers, and air resistance is controlled within a specified range. In this method, a method in which opening of pores is carried out by emulsifying the oil-based compound, but the emulsion is broken when moisture is evaporated at a drying step, and thereby, large pores having a size of 1 μm or more are non-uniformly formed in the sheet. As a result, lithium shielding properties are degraded, and short circuit caused by lithium dendrite easily occurs. For this reason, the aforementioned method cannot be used in lithium ion secondary batteries.

PRIOR ART DOCUMENTS Patent Documents

[Patent Document 1] Japanese Unexamined Patent Application, First Publication No. H11-040130

[Parent Document 2] Japanese Patent No. 4425576

[Patent Document 3] Japanese Patent No. 4201308

[Patent Document 4] Japanese Patent No. 4628764

[Patent Document 5] Japanese Unexamined Patent Application, First Publication No. 2010-090486

SUMMARY OF THE INVENTION Problems to be Solved by the Invention

The present invention was made considering the aforementioned circumstances, and has an objective to provide a porous membrane formed from cellulose, which exhibits a superior performance as a separator, can be prepared at a reasonable cost, exhibits superior strength properties, and can be suitably used as a separator for an electrochemical device.

Means for Solving the Problems

As a result of diligent studies in order to achieve the aforementioned objective, the present inventors discovered that a porous membrane formed from cellulose with specific physical properties exhibits superior performances as a separator for an electrochemical device, thus completing the present invention.

The present invention relates to a porous membrane including cellulose fibers,

wherein a surface area determined by congo red coloring of re-dispersed cellulose fibers curtained after the cellulose fibers of the porous membrane are re-dispersed in accordance with a re-dispersion method for normal paper specimens according to JIS P 8120, ranges from 100 to 300 m²/g.

The aforementioned cellulose fibers are preferably obtained from raw material cellulose fibers having a surface area determined by congo red coloring ranging from 200 to 500 m²/g.

The porous membrane of the present invention preferably has a tensile strength of 50 N·m/g or more.

The porous membrane of the present invention preferably has a porosity ranging from 30 to 70%.

The porous membrane of the present invention is preferably obtained from a slurry containing the aforementioned raw material cellulose fibers together with a hydrophilic pore former.

The solubility of the aforementioned hydrophilic pore former with respect to water is preferably 10% by weight or more.

The aforementioned hydrophilic pore former is preferably a glycol ether.

The aforementioned slurry preferably contains a hydrophilic polymer binder in an amount ranging from 3 to 80 parts by weight with respect to 100 parts by weight of the aforementioned raw material cellulose fibers.

The porous membrane of the present invention preferably has a volume resistivity of 1,500 Ω·cm or less determined by alternate current with a frequency of 20 kHz in which the porous membrane is impregnated with a 1 mol/LiPF₆/propylene carbonate solution.

In addition, the present invention also relates to a process for preparing the aforementioned porous membrane including the steps of:

applying a slurry including at least a hydrophilic pore former and raw material cellulose fibers having a surface area determined by congo red coloring ranging from 200 to 500 m²/g, onto a substrate; drying the aforementioned slurry to form a sheet on the substrate; and separating the sheet from the aforementioned substrate to obtain a cellulose porous membrane formed from the aforementioned sheet.

The process for producing a porous membrane of the present invention preferably further comprises a step of cleaning the aforementioned sheet or the porous membrane with an organic solvent.

Effects of the Invention

The porous membrane formed from cellulose of the present invention exhibits superior performances as a separator for an electrochemical device. Therefore, a separator for an electrochemical device having high lithium shielding properties that cannot be exerted by non-woven fabrics, paper or the like, and at the same time, having a low volume resistivity can be prepared at a reasonable cost by using the aforementioned porous membrane formed from cellulose of the present invention. In addition, the porous membrane formed from cellulose of the present invention has a superior tensile strength, and has superior strength properties as a separator for an electrochemical device.

In addition, in the process for preparing a porous membrane formed from cellulose of the present invention, the pore size and pore amount of the porous membrane formed from cellulose can be freely designed. For this reason, the porous membrane formed from cellulose suitable for a separator for an electrochemical device having high lithium shielding properties that cannot be exerted by non-woven fabrics, paper or the like, and at the same time, having a low impedance or a low volume resistivity can be obtained. In addition, the obtained porous membrane formed from cellulose has superior strength properties, and such a porous membrane formed from cellulose can be prepared at a reasonable cost.

MODES FOR CARRYING OUT THE INVENTION

The porous membrane formed from cellulose or the present invention is a porous membrane including cellulose fibers,

wherein a surface area determined by congo red coloring of cellulose fibers obtained after the cellulose fibers of the porous membrane are re-dispersed in accordance with the re-dispersion method for normal paper specimens according to JIS P 8120, ranges from 100 to 300 m²/g.

In the present invention, usable cellulose fibers are not limited by types of cellulose such as cellulose I, cellulose II, or the like. Natural fibers of cellulose I represented by cotton, cotton linter, or wood pulp are preferable. Fibers of cellulose II represented by regenerated cellulose bare a lower degree of crystallization, as compared with fibers of cellulose I, and tend to form short fibers at the time of subjecting to a fibrillation treatment. Therefore, cellulose II is not preferable.

In the present invention, cellulose fibers may be subjected to microfibrillation. An apparatus for microfibrillation treatment of cellulose fibers is not particularly limited. As examples thereof, mention may be made of, for example, a homogenizer such as a high pressure homogenizer (e.g., high pressure dispersing treatment by a Mantor-Gaulin dispenser), a Ranie type pressure homogenizer, an ultrahigh pressure homogenizer, Altimizer (trademark) (manufactured by Sugino Machine Co., Ltd.), a dispersion apparatus such as a bead mill or a planetary mill, a mass colloider (abrasive grain plate apparatus for grinding in which several abrasive plates provided with abrasive grains having a gram size ranging from No. 16 to No. 120 are arranged for grinding, manufactured by Masuko Sangyo Co., Ltd.) or the like. In addition, a refiner used for papermaking such as a double disk refiner or a beater can also be used for pretreatment before the microfibrillation treatment is carried out. In addition, cellulose nanofibers obtained by forming nanofibers by means of a TEMPO oxidation catalyst can also be used although the blending amount thereof may be limited. In particular, in the present invention, the cellulose fibers are preferably subjected to a pretreatment of a microfibrillation treatment of passing a pulp slurry previously subjected to a refining treatment through a grinding part of a abrasive grain plate apparatus for grinding in which several abrasive plates provided with abrasive grains having a grain sire ranging from No. 16 to No. 120 are arranged for grinding; or a pretreatment of a microfibrillation treatment of subjecting a pulp slurry previously subjected to a refining treatment to a treatment with a high pressure homogenizer.

It is preferable in the present invention that fibers having a diameter of 1 μm or more are contained in an amount of 5% by weight or more, and more preferably 10% by weight or more, with respect to the total weight of the cellulose fibers used in the present invention. In particular, in the preparation process of the present invention described below, casting application is carried out on a substrate, and for this reason, it is difficult to prepare and use a slurry only with thin cellulose fibers having a fiber diameter of less than 1 μm which may cause an extremely high viscosity of the slurry. In addition, in order to make it applicable, the concentration of the slurry must be reduced, and thereby, a cost for drying a solvent used therefor increases. For this reason, a cost may become unreasonable. In addition, if thin cellulose fibers having a reduced fiber diameter are produced by exerting shearing force to cellulose fibers by a general method, the length of fibers also tends to be reduced. Therefore, a strength such as a tear strength of the prepared sheet may tend to be reduced. For this reason, the tear strength of the prepared sheet can be improved by means of the presence of fibers having a diameter of 1 μm or more in an amount of 5% by weight or more. As fibers other than the fibers having a diameter of 1 μm or more, thin nanofibers having a diameter of several nanometers can also be used as long as the casting application can be carried out with the viscosity in a slurry concentration of 1% by weight or more. The upper limit of the amount of the fibers having a diameter of 1 μm or more in the cellulose fibers used in the present invention is not particularly limited. For example, the aforementioned amount may be 40% by weight or less, preferably 30% by weight or less, and more preferably 20% by weight or less. If the fibers having a diameter of 1 μm or more are present in an amount exceeding the specified amount, the number of contact points of individual cellulose fibers via hydrogen bonds is reduced. For this reason, the strength of the obtained sheet may be reduced.

Cellulose fibers can be uniformly dispersed in water by virtue of hydroxyl groups which cellulose molecules have, and the viscosity of the slurry depends on the fiber length and surface area of the cellulose fibers. If cellulose fibers are thinner, the surface area of the cellulose increases, and for this reason, the viscosity of the slurry naturally increases. In addition, as the fiber length becomes longer, interaction among fibers increases. It is believed that this may also be a factor of increasing the viscosity. The increase of viscosity due to the aforementioned interactions is a factor of inhibiting formation of a sheet at a high concentration. In the case of using nanocellulose, a means for reducing a concentration is generally carried out.

In addition, cellulose fibers have a property in which fibers are hydrogen-bonded during the dehydration step by virtue of the hydroxyl groups thereof. This feature cannot be observed in non-woven fabrics prepared with synthetic fibers other than regenerated cellulose. During the aforementioned step of formation of hydrogen bonds, strength is exhibited. On the other hand, shrinkage of cellulose fibers during a drying step due to interactions among fibers is larger than that of non-woven fabrics using synthetic fibers. In particular, as the diameter of fibers becomes thinner, stiffness of the fibers reduces. For this reason, the aforementioned shrinkage is remarkably observed. In addition, it is known that in a sheet prepared using fibers in which fibrillation extremely proceeds, the fibers completely adhere, and for this reason, transparency occurs. Namely, it is difficult to control a pore diameter or produce a porous sheet only by reducing the fiber diameter (thickness). For this reason, control of shrinkage during drying and inhibition of hydrogen bonding among fibers are needed in the production of the porous sheet. Particular conventional methods propose that the raw materials subjected to a sheet formation by means of a papermaking method or a casting method are dried by replacing the solvent with a hydrophilic solvent such as acetone, and subsequently, replacing the hydrophilic solvent with a more hydrophobic solvent such as a solvent mixture of toluene and acetone. However, the aforementioned methods have two problems. The first problem is the operation of solvent replacement of water of the dispersion solvent with acetone. Cellulose fibers exhibit an increased property of maintaining water as the fiber diameter is reduced. For this reason, the replacement of water with the solvent is extremely slow work, and is a factor of reducing productivity in view of practical production. In addition, the pore diameter depends on the diameter of the fibers, and for this reason, the pore diameter is consistently controlled by the thickness of the fibers. Therefore, if uniform fibers are not utilized, the desirable pore diameter cannot be obtained. The step of treating cellulose fibers also requires cost and time.

The fiber length and the fiber diameter of cellulose fibers used when common paper is prepared can be measured by means of a pulp analyzer. It is not easy to evaluate the physical properties of microfibrillated cellulose fibers themselves. For example, in a raw material of fibers in which the diameter of the fibers is microfibrillated to about a few hundred nanometers, the fiber length and the fiber diameter exceed the detection limits, and for this reason, measurement thereof cannot be carried out. In many cases, the evaluation thereof is carried out by visual observation using an electronic microscope. The aforementioned evaluation is carried out in a subjective way by an observer. For this reason, there are problems in that the measurement lacks objectivity, and it is difficult to evaluate a correlation with other physical properties.

Therefore, as a method for objectively evaluating physical properties of microfibrillated cellulose, a method for evaluating a surface area of microfibrillated cellulose by measuring the maximum adsorption amount of a molecule of which the molecular size is known is reported. For example, in Hiroshi Ougiya et. al., relationship between the physical properties and surface area of cellulose derived from adsorbates of various molecular sizes, Biosci. Biotechnol. Biochem., 62 (10), 1880-1884, 1998, it is reported that the surface area of a cellulose raw material such as bacterial cellulose, microfibrillated cellulose (MFC) or the like is measured by measuring an adsorption amount of congo red or various enzymes, and there is a correlation between the aforementioned surface area values and the physical properties such as a viscosity at the time of dispersing fibers, a yield amount of a loading material, and the like. In the present invention, in accordance with the method described in Hiroshi Ougiya et. al., Relationship between the physical properties and surface area of cellulose derived from adsorbates of various molecular sizes, Biosci. Biotechnol. Biochem., 62 (10), 1880-1884, 1998, cellulose fibers are colored with congo red, and the surface area of the aforementioned cellulose is determined by using the amount of congo red adsorbed to the aforementioned cellulose fibers (in the specification of the present application, this is referred to as “congo red coloring”).

The porous membrane formed from cellulose of the present invention has a surface area determined by congo red coloring of cellulose fibers obtained after the cellulose fibers of the porous membrane are re-dispersed in accordance with the re-dispersion method for normal paper specimens according to JIS P 8120, ranges from 100 to 300 m²/g, preferably ranges from 120 to 280 m²/g, and more preferably ranges from 150 to 250 m²/g.

When cellulose fibers are re-dispersed, cleaning is preferably appropriately carried out within a range which does not impair the cellulose fibers in order to remove the additives such as a binder and the like contained in the sheet. The cleaning method is not particularly limited. For example, a method in which filtration is carried out by means of a filter paper, a glass filter, a membrane filter or the like, or a method in which a centrifugal separator is used can be utilized. In addition, an organic solvent such as alcohol, other than water, can be utilized in accordance with types of the additives.

In addition, the cellulose fibers constituting the porous membrane formed from cellulose of the present invention are preferably obtained from, as a raw material, cellulose fibers having a surface area determined by congo red coloring which ranges from 200 to 500 m²/g, preferably ranges from 230 to 470 m²/g, and more preferably ranges from 250 to 450 m²/g.

The porous membrane formed from cellulose of the present invention can have superior strength properties. More particularly, the tensile strength of the porous membrane formed from cellulose of the present invention can be 50 N·m/g or more. The tensile strength can be measured in accordance with JIS C2151. The tensile strength is preferably 55 N·m/g or more, and more preferably 60 N·m/g or more. The porous membrane formed from cellulose of the present invention exhibits a high tensile strength and superior operation ability, since the surface area of the re-dispersed cellulose fibers measured by congo red coloring after cellulose fibers are re-dispersed in accordance with the re-dispersion method for normal paper specimens according to JIS P 8120, ranges from 100 to 300 m²/g.

In addition, the tear strength of the porous membrane formed from cellulose of the present invention can be 0.45 kN/m or more. The tear strength can be measured by means of a Trouser tear method in accordance with JIS K7128-1. The tear strength is preferably 0.5 kN/m or more, more preferably 0.55 kN/g or more, and further more preferably 0.6 kN/m or more. In conventional cellulose membranes for a separator of an electrochemical device, it is difficult to have both a superior tensile strength and a superior tear strength. On the other hand, in the present invention, both a superior tensile strength and a superior tear strength can be exhibited, since the surface area of the re-dispersed cellulose fibers measured by congo red coloring after cellulose fibers are re-dispersed in accordance with the re-dispersion method for normal paper specimens according to JIS P 8120, ranges from 100 to 300 m²/g.

The pore diameter of the porous membrane formed from cellulose of the present invention preferably has the maximum value of the pore diameter measured by a mercury penetration method, which is 1.5 μm or less. The particle size of the electrode active material used in an electrochemical device such as a lithium ion battery varies. For this reason, the pore diameter does not have to be always small. In accordance with an approximate criterion, if the pore diameter is ¼ of the particle size of the electrode active material used in a battery, short circuit may not occur. On the other hand, in the case of use in an electrochemical device which uses active materials having a small particle size, the maximum value must be reduced to be less than 1.5 μm in some cases. When a particle size distribution of the sheet prepared in the present invention is measured by means of a mercury penetration method, a peak can also be identified at 1.5 μm or more. This value is caused by the irregularities of the surface of the sheet, and does not indicate the pore diameter of the porous membrane formed from cellulose.

In the porous membrane formed from cellulose of the present invention, an air resistance per 10 μm of a film thickness preferably ranges from 20 to 600 seconds (/100 cc), more preferably ranges from 20 to 450 seconds, and more preferably ranges from 30 to 250 seconds. The aforementioned air resistance can be measured based on JIS P8117. When the aforementioned air resistance is below 20 seconds, lithium shielding properties are reduced, and risk of occurrences of short circuit due to lithium dendrite may increase for use in lithium ion secondary batteries. Therefore, this is not preferable in view of safety. On the other hand, when the aforementioned air resistance exceeds 600 seconds, the volume resistivity particularly increases, and output properties of the electrochemical device may be degraded. Therefore, this is not preferable.

The porous membrane formed from cellulose of the present invention has a volume resistivity of 1500 Ω·cm or less determined by alternate current with a frequency of 20 kHz in which the porous membrane formed from cellulose is impregnated with a 1 mol/L solution of LiPF₆ dissolved in propylene carbonate. The volume resistivity correlates with the aforementioned air resistance and porosity. Basically, as an air resistance decreases and a porosity increases, a volume resistivity tends to reduce. A pore size of a porous membrane and a pore distribution in the membrane also have effects on a volume resistivity. For this reason, a porous membrane formed from cellulose with a decreased air resistance and an increased porosity does not always exhibit a low volume resistivity. Here, the alternate current with a frequency of 20 kHz is utilized in order to remove an electrochemical element such as a reaction at the electrode interface from the measurement value of the volume resistivity. Thereby, only the total of the resistance of the measurement apparatus and the ion conduction of the porous membrane formed from cellulose contributes to the measurement value. Therefore, the aforementioned measurement value can reflect the pore distribution and pore diameter or the porous membrane formed from cellulose. In particular, the aforementioned volume resistivity is preferably 1,500 Ω·cm or less, and more preferably 1,000 Ω·cm or less. When the volume resistivity exceeds 1,500 Ω·cm, the cycle characteristics may be degraded. When the volume resistivity is 1,500 Ω·cm or less, good cycle characteristics are exhibited. For this reason, such a volume resistivity can be suitable for use as a separator for an electrochemical device.

The measurement of the volume resistivity with the alternate current of 20 kHz in the present invention can be carried out in accordance with the following procedures: First, a porous membrane formed from cellulose punched in a size of 20 mm in diameter is dried for 24 hours or more at 150° C. Subsequently, five dried porous membranes formed from cellulose are placed in a stacking manner in a sample holder for solid of SH2-Z model (manufactured by Toyo Corporation), and then impregnated sufficiently with an electrolytic solution of LiPF₆/propylene carbonate at the concentration of 1 mol/L. In addition, preferably, after the air remaining among porous membranes formed from cellulose is deaerated under reduced pressure which is down to 0.8 MPa, the porous membranes formed from cellulose are bookended between two faced gold electrodes, and alternating current impedance (Ω) is measured by means of a frequency response analyzer VSP (manufactured by Bio-Logic) in which a potentio/galvanostat is combined under the conditions of a swept frequency ranging from 100 mHz to 1 MHz and an amplitude of 10 mV. A resistivity per unit volume (volume resistivity) is obtained from the aforementioned value and the measured thickness of the porous membrane formed from cellulose. It is preferable that only the resistance component, which the measurement apparatus has, be measured or be cancelled so as to non-reflect on the measurement results.

The porosity of the porous membrane formed from cellulose of the present invention preferably ranges from 30% to 70%. The porous membrane formed from cellulose of the present invention maintains the porosity in the range of 30% to 70%, and thereby, the porous membrane formed from cellulose can be applied well to an electrochemical device. Even if the porosity is below 30%, the electrochemical device with the porous membrane formed from cellulose can be operated, but output reduces due to a high resistance value. Therefore, the sufficient performance as the electrochemical device may not be exhibited. On the other hand, if the porosity exceeds 70%, the mode diameter of the pore distribution increases, and resistance caused by the porous membrane formed from cellulose reduces. For this reason, output performances of the electrochemical device and cycle characteristics are improved. However, for use in lithium ion secondary batteries, lithium shielding properties are reduced, and risk of occurrences of short circuit due to lithium dendrite may increase. Therefore, this is not preferable in view of safety.

The porosity in the present invention can be calculated from the weight of the solvent absorbed in the porous membrane formed from cellulose after the porous membrane formed from cellulose is impregnated with the solvent by which the cellulose fibers are not swollen. More particularly, a sample prepared by cutting a separator into a size of 50 mm×50 mm is moisturized for one day under an atmosphere of 23° C. and 50% relative humidify, and subsequently, a thickness of the sample is measured. In addition, the weight of the sample is also weighed by means of a scale defining a 4-digit or 5-digit number. After weighing the sample, the sample is impregnated with a solvent for one minute. Subsequently, the superfluous solvent present over the surface of the sample is removed with absorbent paper, and the weight of the sample is again weighed. A value obtained by subtracting the weight of the sample before impregnation with the solvent from the weight of the sample after impregnation with the solvent, is divided by the density of the solvent. Thereby, a volume of the solvent can be obtained. The obtained value of the volume is divided by the total volume calculated from the thickness, and then multiplied by 100 (%). The obtained value defines porosity. Therefore, the porosity in this case can be obtained from the following equation:

Porosity (%)=100×((weight of sheet after impregnation with solvent)−(weight of sheet before impregnation with solvent))/((density of solvent for use in impregnation)×5×5×(thickness) (cm))

A solvent which can be used in measuring a porosity in the present invention is a solvent by which cellulose is not swollen. For this reason, an organic solvent having a low polarity is preferably used. In addition, the solvent should be selected from solvents which do not evaporate during a short period of time for the measurement. As examples of particularly preferable solvents, mention may be made of propylene glycol usually used in an electrolytic solution or a petroleum-based solvent having a high boiling point such as kerosene, and the like.

The surface roughness Ra of both the front and back sides of the porous membrane formed from cellulose for an electrochemical device prepared in accordance with the present invention is preferably 1.5 or less. It is known that the surface roughness affects the alternating current impedance as contact resistance of the separator and the positive electrode at the time of preparing the electrochemical device. The aforementioned contact resistance can be calculated from the difference between an alternating current impedance value at a frequency of 0.1 Hz and an alternating current impedance value at a frequency of 20,000 Hz, both being measured by means of an electrochemical device such as a laminate cell or a coin battery. As the value of the surface roughness Ra increases, the difference between the alternating current impedance value at 0.1 Hz and the alternating current impedance value at 20,000 Hz increases. The alternating current impedance value is inversely proportional to a facing area in accordance with Ohm's law. When the facing area increases, the measured value itself reduces. For this reason, the measured value tends to be affected by the measurement errors, and the resistance components of the positive electrode and negative electrode are also included in the alternating current impedance value, as the frequency reduces. Therefore, the values cannot be assigned only by the difference of the separator. If a battery having the same electrodes, the same electrolytic solution, and the same size is used, the differences affected by the surface properties of the separators can be observed. For example, the alternating current impedance value at the Ra value of 1.5 is about 1Ω, in the case of a laminate cell having a facing area of 15 cm² prepared by using raw materials for use in a common lithium ion secondary battery, for example, a CoLiO₂-based positive electrode, a graphite-based negative electrode, and an electrolytic solution of LiPF₆. Since a contact resistance of a battery is preferably reduced, the conditions in which Ra is as small as possible are preferable. When a battery is prepared and an alternating current impedance is measured, it is preferable that the impedance be measured after 3 to 5 charge and discharge cycles are carried out at low rates and subsequently, charging is carried out up to a specified electric voltage.

The surface roughness Ra varies in accordance with the effects of the size of the raw materials, the dispersion conditions of the fibers, and the surface properties of the substrates. In particular, the surface roughness Ra is more remarkably affected by the substrate transfer face of the separator, as compared with the size of the raw materials, or the dispersion conditions of the fibers. For this reason, the aforementioned face can be suitably used at the positive electrode side. In the case of using a filter fabric or a wire mesh in a papermaking method, the wire mesh is not appropriate since the transfer face of the filter fabric appears as it is, and the Ra value cannot be controlled to a small value.

The porous membrane formed from cellulose of the present invention can be obtained by a slurry containing the aforementioned raw material cellulose fibers. The aforementioned slurry has a viscosity which is preferably less than 3,000 cps, is more preferably 2,500 cps or less, and is further more preferably 2,000 cps or less, in the case of measuring by means of a Brookfield viscometer (number of rotation=60 rpm) at 25° C.

The porous membrane formed from cellulose of the present invention can be preferably obtained in accordance with a process for preparing a porous membrane at least including the steps of:

applying a slurry including at least a hydrophilic pore former and raw material cellulose fibers having a surface area determined by congo red coloring ranging from 200 to 500 m²/g, onto a substrate; drying the aforementioned slurry to form a sheet on the substrate; and separating the sheet from the aforementioned substrate to obtain a cellulose porous membrane formed from the aforementioned sheet.

In the preparation process of the present invention, as a means for making a sheet formed from cellulose fibers porous, a slurry including a hydrophilic pore former is applied onto a substrate, followed by drying. Thereby, production efficiency can be greatly improved. In addition, in the present invention, solubility of the hydrophilic pore former with respect to water is adjusted, and thereby, a pore size of the sheet can be controlled. In addition, in the present invention, the blending amount of the hydrophilic pore former is adjusted, and thereby, porosity can be freely controlled. For example, in the present invention, the hydrophilic pore former can be used in an amount preferably ranging from 50 to 600 parts by weight, more preferably ranging from 80 to 400 parts by weight, and further preferably ranging from 100 to 300 parts by weight, with respect to 100 parts by weight (mass) of the cellulose fibers.

The hydrophilic pore former used in the present invention is not particularly limited as long as it is a hydrophilic substance which can form pores in the sheet formed from cellulose fibers. The boiling point of the hydrophilic pore former is preferably 180° C. or more. It is known that hydrogen bonding among the fibers occurs when the moisture of the sheet ranges from 10 to 20% by weight during drying. At the time of forming the aforementioned hydrogen bonds, the pore former is present in the sheet, and the hydrogen bonding among fibers is inhibited. Thereby, a porous sheet can be produced. In the case of using a pore former having a boiling point of less than 180° C., the pore former evaporates during the drying step even if the blending amount thereof is increased, and sufficient formation of a porous sheet may not be carried out. For this reason, a pore former having a boiling point of 180° C. or more is preferable. The pore former preferably has a boiling point of 200° C. or more. A primary alcohol or the like having a molecular weight which is less than that of hexanol is a material having both water solubility and hydrophobic properties. Such a material easily evaporates as compared with water during the drying step, and for this reason, hydrogen bonding cannot be sufficiently inhibited. Therefore, it cannot be used in the present invention. With the proviso of using a drying method under specific conditions different from the usual drying conditions, such as drying with the air filled with vapor of the pore former, or using multi-stage drying with a solvent having a lower vapor pressure than that of water, the pore former does not necessarily have a boiling point of 180° C. or more.

The hydrophilic pore former used in the present invention has a solubility with respect to water which is preferably 20% by weight or more, and more preferably 30% by weight or more. In the case of using a pore former having a solubility with respect to water of less than 20% by weight, the blending amount of the pore former is limited. For this reason, it may be difficult to control the desirable porosity only by the blending amount of the pore former. In addition, as drying proceeds, the amount of the solvent reduces, and thereby, the pore former which cannot be dissolved is separated. For this reason, it may be difficult to uniformly form pores in the face direction and the thickness direction of the sheet. The aforementioned hydrophobic pore former may be emulsified with an emulsifier or the like, and thereby, pores can be formed, uniformly to some extent. However, it is difficult to control the pore diameter. On the other hand, in the case of using a pore former having a solubility with respect to water of 20% by weight or more, the pore former can be uniformly dispersed in the slurry, and as a high solubility with respect to water is exhibited, separation does not occur during the drying step. For this reason, by uniformly inhibiting hydrogen bonding in the drying step, pores can be uniformly produced.

The hydrophilic pore former used in the present invention has a vapor pressure at live which is preferably less than 0.1 kPa, more preferably less than 0.09 kPa, and further more preferably less than 0.08 kPa. A hydrophilic pore former having a vapor pressure of 0.1 kPa or more has an increased volatility. For this reason, such a hydrophilic pore former highly tends to vaporize before the pore former contributes to form pores for a cellulose membrane. As a result, it may be difficult to obtain a porous cellulose membrane.

The hydrophilic pore former used in the present invention has a water-octanol partition coefficient (Log Pow) preferably ranging from −1.2 to 0.8, more preferably ranging from −1.1 to 0.8, and further more preferably ranging from −0.7 to 0.4. As the aforementioned octanol, n-octanol is preferable. If a hydrophilic pore former having the aforementioned partition coefficient of less than −1.2 is used, an impedance value of the obtained porous membrane formed from cellulose may increase.

As examples of hydrophilic pore formers which can be used in the present invention, mention may be made of, for example, a higher alcohol such as 1,5-pentanediol, 1-methylamino-2,3-propanediol, or the like; a lactone such as ε-caprolactone, α-acetyl-γ-butyrolactone, or the like; a glycol such as diethylene glycol, 1,3-butylene glycol, propylene glycol, or the like; and a glycol ether such as triethylene glycol dimethyl ether, tripropylene glycol dimethyl ether, diethylene glycol monobutyl ether, triethylene glycol monomethyl ether, triethylene glycol butyl methyl ether, tetraethylene glycol dimethyl ether, diethylene glycol monoethyl ether acetate, diethylene glycol monoethyl ether, triethylene glycol monobutyl ether, tetraethylene glycol monobutyl ether, dipropylene glycol monomethyl ether, diethylene glycol monomethyl ether, diethylene glycol monoisopropyl ether, ethylene glycol monoisobutyl ether, tripropylene glycol monomethyl ether, diethylene glycol methyl ethyl ether, diethylene glycol diethyl ether or the like, as well as glycerol propylene carbonate; N-methylpyrrolidone; or the like. Examples thereof are not limited thereto. Among these, glycol ethers have a low vapor pressure, and are the most preferable in the preparation process of the present invention.

The slurry used in the present invention preferably contains, in addition to the raw cellulose fibers and the hydrophilic pore former, a hydrophilic polymer binder as an adhesive for linking the fibers in an amount ranging from 3 to 80 parts by weight, and preferably ranging from 5 to 50 parts by weight with respect to 100 parts by weight of the aforementioned cellulose fibers. The hydrophilic polymer binder can exhibit a function of improving properties of dispersing cellulose, in addition to the function as an adhesive. In order to obtain a uniform pore distribution, fibers are necessary for being uniformly dispersed in the slurry. The hydrophilic polymer binder fixes to the surface of the cellulose fibers to have a role like a protective colloid. For this reason, dispersion properties are improved. If the blending amount of the binder is less than 3 parts by weight, strength of the obtained sheet may be degraded, and dispersion properties of the cellulose fibers may be impaired. For this reason, it is difficult to obtain uniform pores. On the other hand, if the amount exceeds 80 parts by weight, the binder fills in pores, and the volume resistivity of the porous membrane formed from cellulose is increased. Therefore, they are not preferable.

As the aforementioned hydrophilic polymer binder, a cellulose derivative such as methylcellulose, carboxymethylcellulose, hydroxyethylcellulose, hydroxypropylcellulose, hydroxypropylmethylcellulose, hydroxyalkylcellulose or the like; a derivative of a polysaccharide such as phosphate starch, cationated starch, corn starch or the like; or a binder such as a styrene butadiene copolymer emulsion, polyvinylidene fluoride or the like, known as a binder for electrodes can be used.

The substrate used in the present invention is not particularly limited, and a polymer film, a glass plate, a metal plate, a peeling paper or the like can be used therefor. As the substrate, one in which the hydrophilic pore former in the slurry is not dropped from the rear face of the substrate, such as a wire, a filter fabric, a paper filter or the like is preferable. In the preparation process of the present invention, pores are formed using the hydrophilic pore former. For this reason, if the hydrophilic pore former is removed from the rear face of the substrate during the drying step, pores cannot be sufficiently formed on the sheet. In addition, the dried sheet has characteristics in that the surface property of the substrate is transferred. For this reason, the surface of the substrate is preferably as smooth as possible. Considering the aforementioned descriptions, a biaxially-drawn polyethylene terephthalate film has flexible properties, and the melting temperature thereof is relatively high. Therefore, effects of stretch or shrinkage during drying can be reduced. In addition, the biaxially-drawn polyethylene terephthalate film exhibits higher polarity, as compared with a polypropylene film. For this reason, the film is easily applied even in an aqueous slurry formulation, and can be suitably used.

In the preparation process of the present invention, as the method for applying she slurry containing the cellulose fibers and the hydrophilic pore former onto the substrate, any means can be used as long as the slurry can be uniformly applied so that the film thickness of the applied layer is within a specified range. For example, the application can be carried out in a pre-metered coater such as a slot die coater, a curtain coater, or the like, or even in an after-metered coater such as an MB coater, an MB reverse coater, a comma coater, or the like.

In the present invention, a surfactant can be added to the slurry as an additive, if necessary. A nonionic surfactant represented by acetylene glycol as a defoamer or a leveling agent can be used in an amount which has no effects on the properties of electrochemical devices. No use of ionic surfactants is preferable since ionic surfactants may affect properties of electrochemical devices.

In the slurry containing the cellulose fibers and the hydrophilic pore former, a loading material can be contained in addition to the aforementioned binder and the aforementioned surfactant. For example, an inorganic loading material such as silica particles or alumina particles, an organic loading material such as silicone powders and the like can be used. These particles can be added in an amount which has no effects on the pores of the porous membrane formed from cellulose. Use of the particles having an average particle size of less than 2 μm is preferable. If the average particle size is 2 μm or more, pores with a large pore diameter are formed by interspace among the particles, and for this reason, this is not preferable. The aforementioned loading materials have effects of reducing the viscosity of the slurry. For this reason, a concentration of the coating material can be increased, and this is suitable for increasing production efficiency. On the other hand, if an excessive amount thereof is used, strength is reduced. For this reason, a blending amount thereof which is more than 100 parts by weight with respect to 100 parts by weight of the cellulose fibers is not preferable.

The solvent of the slurry used in the present invention basically needs use or water. For the purpose of improving drying efficiency, a solvent having a higher vapor pressure than that of water, such as an alcohol such as methanol, ethanol or t-butyl alcohol, a ketone such as acetone or methyl ethyl ketone, an ether such as diethyl ether or ethyl methyl ether or the like can be added in an amount of up to 50% by weight of the total amount of the solvent. If the aforementioned solvents are added in an amount of 50% by weight or more, dispersing properties of the cellulose fibers are impaired, and uniformity of pore distribution is impaired. For this reason, this is not preferable.

In the preparation process of the present invention, the aforementioned slurry applied onto the substrate can be dried to obtain a sheet. The drying method is not particularly limited. In particular, a drying method which is commonly used, such as any one or both of drying with hot air and drying with far-infrared radiation, can be used. For example, the temperature of hot air can range from 30° C. to 150° C., and preferably range from 60° C. to 120° C. It is necessary to adjust the temperature of hot air, the amount of hot air, radiation conditions of far-infrared radiation or the like so that the structure in the thickness direction of the sheet is dried as uniformly as possible, under the conditions of the temperature of hot air, the amount of hot air, and the temperature of far-infrared radiation. In addition, in order to improve a drying efficiency, microwave heating can also be used.

The thickness of the sheet in the present invention preferably ranges from 10 to 40 μm. The thickness of the porous membrane formed from cellulose is a factor which can largely change performance of the electrochemical device. If the thickness is below 10 μm, sufficient lithium shielding properties cannot be exhibited, and safety may be insufficient. On the other hand, if the thickness exceeds 40 μm, the volume resistivity of the porous membrane formed from cellulose is increased, and the output performance of the electrochemical device may be degraded. For this reason, they are not preferable. A sheet having a thickness ranging from 15 to 30 μm is particularly preferable in view of balance between lithium shielding properties and a value of volume resistivity.

In the preparation process of the present invention, the sheet formed onto the substrate as described above is separated, and thereby, a porous membrane formed from cellulose, which is formed from the aforementioned sheet, can be obtained. A method of separating a porous membrane formed from a substrate is not particularly limited.

The preparation process of the present invention can further have a step of cleaning the aforementioned sheet with an organic solvent, in addition to the steps of applying a slurry including at least a hydrophilic pore former and raw material cellulose fibers having a surface area determined by congo red coloring ranging from 200 to 500 m²/g, onto a substrate; drying the aforementioned slurry to form a sheet on the substrate; and separating the sheet from the aforementioned substrate to obtain a cellulose porous membrane formed from the aforementioned sheet. The aforementioned cleaning step is carried out in order to remove components inhibiting performances of the electrochemical device in the case of using a surfactant, if necessary, and smoothly carry out separating the aforementioned sheet from the substrate. The organic solvent is not limited as long as the organic solvent can be used in the cleaning step. A hydrophobic solvent with a reduced solubility with respect to water is preferable in order to avoid effects of shrinkage of the sheet due to movement of the residual moisture in the organic solvent.

With respect to the aforementioned organic solvent, for example, one or two or more types of organic solvents having a relatively high evaporating rate such as acetone, methyl ethyl ketone, ethyl acetate, n-hexane, toluene, or propanol can be used once or in several divided applications. The usage manner of the organic solvent is not limited thereto. For the purpose of removing the residual pore former, a solvent with high compatibility with water, such as ethanol or methanol is preferable. However, moisture in the sheet moves to the solvent or moisture in the air absorbs to affect physical properties of the porous membrane formed from cellulose or the form of the sheet. For this reason, such a solvent must be used under the conditions in which the moisture amount is controlled. A solvent which is highly hydrophobic such as n-hexane or toluene exhibits poor effects of cleaning the hydrophilic pore former, but it is difficult to absorb moisture. For this reason, such a solvent can be preferably used. From the reasons described above, for example, a method in which cleaning is carried out successively with some solvents, for example, acetone, toluene, and n-hexane in order of gradually increasing the hydrophobic properties of the solvents, and the successive cleaning is repeated to replace the solvent, is preferable.

The porous membrane formed from cellulose of the present invention can be used as care constitutional element of a separator for an electrochemical device, or can be used as it is, as a separator for an electrochemical device.

The separator for an electrochemical device of the present invention can be used in, for example, a battery such as a lithium ion secondary battery or a polymer lithium battery, as well as a capacitor such as an aluminum electrolytic capacitor, an electrical double-layered capacitor, or a lithium ion capacitor.

The constitution of the aforementioned electrochemical device can be exactly the same as that of a conventional electrochemical device, with the exception of using the aforementioned separator for an electrochemical device of the present invention as a separator. The cell structure of the electrochemical device is not particularly limited. As examples thereof, mention may be made of a laminate type, a cylinder type, a square type, a coin type and the like.

For example, a lithium ion secondary battery as the electrochemical device comprising the separator of the present invention has a positive electrode and a negative electrode, between which the aforementioned separator for an electrochemical device is arranged, and the aforementioned separator for an electrochemical device is impregnated with an electrolytic solution.

The aforementioned positive electrode and negative electrode contain electrode active materials. As a positive electrode active material, a conventionally known one can be used. As examples thereof, mention may be made of, for example, a lithium transition metal oxide such as LiCoO₂, LiNiO₂, or LiMn₂O₄; a lithium metal phosphate such as LiFePO₄; and the like. As a negative electrode active material, a conventionally known one can be used. As examples thereof, mention may be made of, for example, a carbon material such as graphite; a lithium alloy; and the like. In addition, conventionally known conductive auxiliary materials or binders can be added in the electrodes, if necessary.

For the preparation of a lithium ion secondary battery, first, a positive electrode mixture containing a positive electrode active material and, if necessary, a conventionally known conductive auxiliary material and/or a conventionally known conductive binder, and a negative electrode mixture containing a negative electrode active material and, if necessary, a conventionally known conductive auxiliary material and/or a conventionally known conductive binder, are independently applied on conventionally known collectors. For the collector of the positive electrode, for example, aluminum or the like is used, and for the collector of the negative electrode, copper, nickel, or the like is used. After the positive electrode mixture and the negative electrode mixture are applied onto the collectors, they are dried and subjected to pressure forming. Thereby, a positive electrode in which an active material layer is formed on the collector, and a negative electrode in which an active material layer is formed on the collector can be obtained.

Subsequently, the obtained positive electrode and negative electrode and the separator for an electrochemical device of the present invention are laminated or wound in order of the positive electrode, the separator for an electrochemical device, and the negative electrode to construct a device. Subsequently, the aforementioned device is housed in an exterior material, the collectors are connected to external electrodes, and are impregnated with a conventionally known electrolytic solution. Subsequently, the exterior material is sealed. Thereby, a lithium ion secondary battery can be obtained.

In addition, an electrical double-layered capacitor as the electrochemical device comprising the separator of the present invention has a positive electrode and a negative electrode, between which the separator for an electrochemical device of the present invention is arranged, and the aforementioned separator for an electrochemical device is impregnated with an electrolytic solution.

The electrodes of the aforementioned positive electrode and negative electrode can be obtained by, for example, applying an electrode mixture containing activated carbon powder and a conventionally known conductive auxiliary material and/or conventionally known conductive binder onto a conventionally known collector, drying and subjecting to pressure forming. As the collector, for example, aluminum or the like is used.

The electrical double-layered capacitor can be obtained as follows: the positive electrode and negative electrode and the separator for an electrochemical device of the present invention are laminated or wound in order of the positive electrode, the separator for an electrochemical device, and the negative electrode to construct a device. Subsequently, the aforementioned device is housed in an exterior material, and the collectors are connected to external electrodes, and are impregnated with a conventionally known electrolytic solution. Subsequently, the exterior material is sealed.

EXAMPLES

Hereinafter, the present invention is described in detail with reference to Examples and Comparative Examples. It should be understood that the scope of the present invention is not limited to these Examples.

(1) Measurement of Fiber Length

The number average fiber length was measured by means of a fiber length-measuring machine, FIBER TESTER (manufactured by L & W).

(2) Measurement of Thickness

The thickness of the separator sample with a size of 50 mm×50 mm was measured at any 5 points by means of a thickness indicator TM600 (manufactured by Kumagai Riki Kogyo Co., Ltd.). An average value obtained from the aforementioned 5 values of thickness measured was used as a membrane thickness.

(3) Measurement of Tensile Strength

The tensile strength was measured by means of a method in accordance with JIS C2151.

(4) Measurement of Alternating Current Impedance at Frequency of 20 kHz and Determination of Volume Resistivity

A sample holder for solid of SH2-Z model (manufactured by Toyo Corporation) was used as a cell for measuring impedance. A separator punched in a size of a 20 mm diameter was dried for 24 hours or more trader the condition of 150° C. Subsequently, five dried separators were placed therein in a stacking manner, and then impregnated sufficiently with a 1 mol/L electrolytic solution of LiPF₆/propylene carbonate. After the air remaining among separators was deaerated under reduced pressure which was down to 0.8 MPa, the separators were bookended between two faced gold electrodes, and an alternating current impedance (Ω) was measured by means of a frequency response analyzer VSP (manufactured by Bio-Logic) in which a potentio/galvanostat was combined under the conditions of a swept frequency ranging from 100 mHz to 1 MHz and an amplitude of 10 mV. The measurement temperature was 25° C. A resistivity (volume resistivity) per unit volume was obtained from the aforementioned value and the thickness measured in the aforementioned (2).

(5) Re-Dispersion of Porous Membrane Formed from Cellulose

A porous membrane formed from cellulose was sampled in an amount of 0.5 g, and 49.5 g of ion-exchanged water was added thereto. The mixture was heated until the temperature of water was heated to 60° C. Subsequently, the mixture was stirred for 10 minutes at 7,000 rpm by means of a homomixer (CELL MASTER CM-100, manufactured by AS ONE Corporation). Thereby, re-dispersion of the porous membrane formed from cellulose was carried out. The obtained dispersion was cleaned with a glass filter, and subsequently, subjected to congo red coloring.

(6) Measurement of Surface Area by Congo Red Coloring

The measurement of the surface area by congo red coloring was carried out in accordance with a method described in Hiroshi Ougiya et. al., Relationship between the physical properties and surface area of cellulose derived from adsorbates of various molecular sizes., Biosci. Biotechnol. Biochem., 62 (10), 1880-1884, 1998. More particularly, microfibrillated fibers were dispersed in 50 ml of a phosphate buffer (pH 6) so that the concentration of cellulose was 0.1% by weight. The dispersions together with various concentrations of congo red were maintained for 12 hours at 30° C. Subsequently, the suspension was subjected to centrifugation for 10 minutes at 3,000 rpm. The amount of congo red in the supernatant was obtained by measuring absorbance at 492 nm. The maximum adsorption amount of congo red was obtained in accordance with the following equation (1) derived from a Langmuir adsorption theory.

[E]/[A]−1/(K _(ad) [A] _(max))+(1/[A] _(max))[E]  (1)

[E]: Congo red concentration (mg/ml) at equilibrium; [A]: Congo red amount (g/g of cellulose) adsorbed on the surface of cellulose; K_(ad): Equilibrium constant; and [A]_(max): Maximum adsorption amount of congo red (g/g of cellulose) adsorbed on the surface of cellulose.

The surface area Ss of microfibrillated cellulose was obtained from [A]_(max) in accordance with the following equation (2). The surface area of cellulose was indicated as the numerical value per 1 g of the solid content of cellulose.

Ss=([A] _(max) ·N·Sa)/(Mw×10²¹)  (2)

Ss: Surface area of cellulose (m²/g of cellulose); Sa: Area covered when one molecule of congo red is adsorbed on the surface (1.73 nm²); N: Avogadro number; and Mw: Molecular weight of congo red.

(7) Measurement of Porosity

A sample prepared by cutting a separator into a size of 50 mm×50 mm was moisturized for one day under an atmosphere of 23° C. and 50% relative humidity, and subsequently, a thickness of the sample was measured and a weight of the sample was weighed by means of a scale defining a 4-digit or 5-digit number. After weighing the sample, the sample was impregnated with kerosene for one minute. Subsequently, the superfluous solvent present over the surface of the sample was removed with absorbent paper, and the weight of the sample was again weighed. The porosity was calculated by the aforementioned equation.

Example 1

NBKP was dispersed in ion-exchanged water so as to have a concentration of 2% by weight. The dispersion was subjected to a refining treatment by cycling under the conditions so that the number average fiber length was 1.0 mm or less, by means of a double disk refiner. The dispersion of the cellulose fibers in which the number average fiber length was 1.0 mm or less was treated five times by means of a high-pressure homogenizer (manufactured as LAB-1000) under the condition of 800 bar. Thereby, a raw material 1 of cellulose fibers was obtained. The surface area of the aforementioned raw material 1 of cellulose fibers measured by congo red coloring was 320 m²/g. The aforementioned raw material 1 of cellulose fibers was subjected to a treatment using a centrifuge machine for 5 minutes under the condition of 10,000 rpm to have a concentration of about 10% by weight.

With respect to 100 parts by weight of the aforementioned raw material 1 of cellulose fibers, 250 parts by weight of triethylene glycol butyl methyl ether having a boiling point of 261° C. and having an infinite solubility with respect to water as a hydrophilic pore former, and 20 parts by weight of carboxymethylcellulose (product name: MAC-500 LC, manufactured by Nippon Paper Industries Co., Ltd., Chemical Division) dissolved in ion-exchanged water to have a concentration of 1% by weight as a binder, were added, and water was added thereto so that the concentration of the solid content of the mixture was finally 1.5% by weight. Thereby, a coating material was prepared. The coating material was subjected to a dispersion treatment by means of a bead mill with zirconia beads with a 3-μm size until the mixture was uniformly mixed.

The prepared coating material was applied onto a PET film having a thickness of 100 μm by means of an applicator so that a WET sheet thickness was 1 mm, and subsequently, dried for 12 minutes by means of hot air at 80° C. and an infrared heater. The obtained coating sheet was separated from the PET film in toluene, and subsequently, toluene was evaporated therefrom. Thereby, a sheet (porous membrane formed from cellulose) having a sheet thickness of 20 μm was obtained.

Example 2

NBKP was dispersed in ion-exchanged water so as to have a concentration of 2% by weight. The dispersion was subjected to a refining treatment by cycling under the conditions so that the number average fiber length was 1.0 mm or less, by means of a double disk refiner. The dispersion of the cellulose fibers in which the number average fiber length was 1.0 mm or less was treated three times by means of a high-pressure homogenizes (manufactured as LAB-1000) under the condition of 800 bar. Thereby, a raw material 2 of cellulose fibers was obtained. The surface area of the aforementioned raw material 2 of cellulose fibers measured by congo red coloring was 240 m²/g. A sheet having a sheet thickness of 20 μm was obtained in the same manner as that of Example 1, with the exception of using 100% by weight of the aforementioned raw material 2 of cellulose fibers.

Example 3

NBKP was dispersed in ion-exchanged water so as to have a concentration of 2% by weight. The dispersion was subjected to a refining treatment by cycling under the conditions so that the number average fiber length was 1.0 mm or less, by means of a double disk refiner. The dispersion of the cellulose fibers in which the number average fiber length was 1.0 mm or less was treated fifteen times by means of a high-pressure homogenizer (manufactured as LAB-1000) under the condition of 800 bar. Thereby, a raw material 3 of cellulose fibers was obtained. The surface area of the aforementioned raw material 3 of cellulose fibers measured by congo red coloring was 450 m²/g. A sheet having a sheet thickness of 19 μm was obtained in the same manner as that of Example 1, with the exception of using 100% by weight of the aforementioned raw material 3 of cellulose fibers.

Example 4

NBKP was dispersed in ion-exchanged water so as to have a concentration of 2% by weight. The dispersion was subjected to a refining treatment by cycling under the conditions so that the number average fiber length was 1.0 mm or less, by means of a double disk refiner. The dispersion of the cellulose fibers in which the number average fiber length was 1.0 mm or less was treated three times by means of a mass colloider (manufactured by Masuko Sangyo Co., Ltd.). Thereby, a raw material 4 of cellulose fibers was obtained. The surface area of the aforementioned raw material 4 of cellulose fibers measured by congo red coloring was 410 m²/g. A sheet having a sheet thickness of 19 μm was obtained in the same manner as that of Example 1, with the exception of using 100% by weight of the aforementioned raw material 4 of cellulose fibers.

Comparative Example 1

NBKP was dispersed in ion-exchanged water so as to have a concentration of 2% by weight. The dispersion was subjected to a refining treatment by cycling under the conditions so that the number average fiber length was 1.0 mm or less, by means of a double disk refiner. The dispersion of the cellulose fibers in which the number average fiber length was 1.0 mm or less was treated twice by means of a high-pressure homogenizer (manufactured as LAB-1000) under the condition of 800 bar. Thereby, a raw material 5 of cellulose fibers was obtained. The surface area of the aforementioned raw material 5 of cellulose fibers measured by congo red coloring was 170 m²/g. A sheet having a sheet thickness of 23 μm was obtained in the same manner as that of Example 1, with the exception of using the aforementioned raw material 5 of cellulose fibers.

Comparative Example 2

NBKP was dispersed in ion-exchanged water so as to have a concentration of 2% by weight. The dispersion was subjected to a refining treatment by cycling under the conditions so that the number average fiber length was 1.0 mm or less, by means of a double disk refiner. The dispersion of the cellulose fibers in which the number average fiber length was 1.0 mm or less was treated 25 times by means of high-pressure homogenizer (manufactured as LAB-1000) under the condition of 800 bar. Thereby, a raw material 6 of cellulose fibers was obtained. The surface area of the aforementioned raw material 6 of cellulose fibers measured by congo red coloring was 530 m²/g. The production of a sheet was tried in the same manner as that of Example 1, with the exception of using the aforementioned raw material 6 of cellulose fibers. However, the slurry was gelled on the mixing stage, and uniformly casting of the slurry onto the PET film could not be carried out. Therefore, the formation of a uniform sheet could not be carried out.

The sheet of each of Examples 1 to 4 and Comparative Examples 1 and 2 was stirred for 10 minutes at 7,000 rpm by means of a homomixer (CELL MASTER CM-100, manufactured by AS ONE Corporation). Thereby, a re-dispersed slurry having a solid content in an amount of 1% by weight was obtained. The surface area of the microfibrillated cellulose fibers in each of the aforementioned re-dispersed slurries was measured by means of congo red coloring in accordance with a method shown in the aforementioned “(6) Measurement of surface area by congo red coloring”.

Various physical properties of the sheets formed from cellulose which were prepared in Examples 1 to 4 and Comparative Examples 1 and 2 are shown in Table 1.

TABLE 1 Surface area Surface at the Mem- area time of brane of raw re-dis- thick- Tensile Volume material persion ness Porosity strength resistivity g/g g/g μm % N·m/g Ω·cm Example 1 320 160 20 45 67.9 750 Example 2 240 110 20 43 53.6 920 Example 3 450 280 19 47 61.5 690 Example 4 410 210 19 47 58.5 870 Comparative 170 80 23 42 23.8 1050 Example 1 Comparative 530 330 A uniform sheet could not be obtained. Example 2

From the results of Examples 1 to 4, it can be seen that the porous membranes formed from cellulose including cellulose fibers with a surface area ranging from 100 to 300 m²/g after re-dispersion, measured by congo red coloring exhibit a tensile strength of 50 N·m/g or more, and porous membranes formed from cellulose for a separator of an electrochemical device, exhibiting a superior strength, can be prepared.

On the other hand, Comparative Example 1 indicates that the porous membrane formed from cellulose including cellulose fibers having the aforementioned surface area of less than 100 m²/g has a reduced tensile strength. In addition, Comparative Example 2 indicates that a porous membrane formed from cellulose including cellulose fibers having the aforementioned surface area exceeding 300 m²/g cannot be prepared.

As an example of an electrochemical device, the performances of a lithium ion secondary battery were verified.

Example 5 Preparation of a Lithium Ion Secondary Battery

A positive electrode was prepared by preparing a combination obtained by mixing LiCoO₂, acetylene black and a Pvdf-NMP solution (polyvinylidene fluoride-N-methylpyrrolidone) in a mass ratio of solid contents of 89:6:5, applying the combination onto an aluminum foil and drying it, casting it under pressure, and subsequently subjecting it to a heat treatment. A negative electrode was prepared by preparing a combination obtained by mixing mesocarbon microbead graphite, acetylene black, and a Pvdf-NMP solution in a mass ratio of solid contents of 90:5:5, applying the combination onto a copper foil and drying it, casting it under pressure, and subsequently subjecting it to a heat treatment.

A lithium ion secondary battery (cell size: 30×50 mm, capacity: 180 mAh) was prepared by using the porous membrane formed from cellulose obtained in Example 1 as a separator, interposing the aforementioned separator between a negative electrode and a positive electrode to form a group of electrodes, and loading an aluminum pack with the aforementioned group of electrodes and a 1 mol/L non-aqueous electrolytic solution obtained by dissolving LiPF₆ in a solvent mixture obtained by mixing ethylene carbonate and diethyl carbonate in a volume ratio of 3:7.

Evaluation of Lithium Ion Secondary Battery

With respect to the lithium ion secondary battery prepared in Example 5, the inner resistivity of the battery was evaluated by the measurement of alternating current impedance. The alternating current impedance (Ω) was measured using a frequency response analyzer 1260 model (manufactured by Solartron Metrology) under the conditions of swept frequency ranging from 10 mHz to 500 kHz and amplitude of 5 mV. A Cole-Cole plot was prepared from the aforementioned measurement values, and a value of a real part was read when a value of an imaginary part was 0. The read value was used as an inner resistivity (Ω). The inner resistivity was 0.121Ω.

As an example of the electrochemical device other than the lithium ion secondary battery, the performances of an electrical double-layered capacitor were verified.

Example 6 Preparation of Electrical Double-Layered Capacitor

An electrode was prepared by preparing a combination obtained by mixing a mixture of activated carbon, acetylene black and tetrafluoroethylene in a mass ratio of the solid content of 10:1:1, applying the combination onto an aluminum foil and drying it, casting it under pressure, and subsequently subjecting it to a heat treatment.

The porous membrane formed from cellulose obtained in Example 1 was used as a separator, and the separator was cut into a size which was larger by about 0.5 mm than the size of the electrode. The electrode was formed so as to nave the facing area of 15 cm². The separator was interposed between two electrodes, and a 1 mol/L solution of tetraethylammonium BF₄ salt (organic electrolyte) in propylene carbonate was filled therein. Thereby, an electrical double-layered capacitor was prepared.

Evaluation of Electrical Double-Layered Capacitor

The performances of the electrical double-layered capacitor prepared in Example 6 were evaluated. The inner resistivity of the battery was evaluated by the measurement of alternating current impedance. The alternating current impedance (Ω) was measured using a frequency response analyzer 1260 model (manufactured by Solartron Metrology) under the conditions of swept frequency ranging from 10 mHz to 500 kHz and amplitude of 5 mV. A Cole-Cole plot was prepared from the aforementioned measurement values, and a value of a real part was read when a value of an imaginary part was 0. The read value was used as an inner resistivity (Ω). The inner resistivity was 0.060Ω.

As described above, from the results of Example 5 and Example 6, it can be seen that the battery and the capacitor equipped with the porous membranes formed from cellulose of the present invention have a reduced inner resistivity, and can be suitably used as a battery or a capacitor. 

1. A porous membrane comprising cellulose fibers, wherein a surface area determined by congo red coloring of re-dispersed cellulose fibers obtained after the cellulose fibers of the porous membrane are re-dispersed in accordance with a re-dispersion method for normal paper specimens according to JIS P 8120, ranges from 100 to 300 m²/g.
 2. The porous membrane according to claim 1, wherein said cellulose fibers are obtained from raw material cellulose fibers having a surface area determined by congo red coloring ranging from 200 to 500 m²/g.
 3. The porous membrane according to claim 1, having a tensile strength which is 50 N·m/g or more.
 4. The porous membrane according to claim 1, having a porosity ranging from 30 to 70%.
 5. The porous membrane according to claim 2, which is prepared from a slurry containing a hydrophilic pore former together with said raw material cellulose fibers.
 6. The porous membrane according to claim 5, wherein a solubility of said hydrophilic pore former with respect to water is 10% by weight or more.
 7. The porous membrane according to claim 5, wherein said hydrophilic pore former is a glycol ether.
 8. The porous membrane according to claim 5, wherein said slurry contains a hydrophilic polymer binder in an amount ranging from 3 to 80 parts by weight with respect to 100 parts by weight of said raw material cellulose fibers.
 9. The porous membrane according to claim 1, which has a volume resistivity of 1,500 Ω·cm or less determined by alternate current with a frequency of 2.0 kHz in which the porous membrane is impregnated with a 1 mol/LiPF₆/propylene carbonate solution.
 10. A separator for an electrochemical device comprising the porous membrane as recited in claim
 1. 11. An electrochemical device comprising the separator for an electrochemical device as recited in claim
 10. 12. The electrochemical device according to claim 11, which is one of a battery and a capacitor.
 13. A process for preparing a porous membrane formed from cellulose comprising the steps of: applying a slurry including at least a hydrophilic pore former and raw material cellulose fibers having a surface area determined by congo red coloring ranging from 200 to 500 m²/g, onto a substrate; drying said slurry to form a sheet on the substrate; and separating said sheet from said substrate to obtain a cellulose porous membrane formed from said sheet.
 14. The process for preparing the cellulose porous membrane according to claim 13, further comprising a step of cleaning said sheet or porous membrane with an organic solvent. 